JP2001302222A - Ammonium polyphosphate with improved fluidity and method for producing the same - Google Patents
Ammonium polyphosphate with improved fluidity and method for producing the sameInfo
- Publication number
- JP2001302222A JP2001302222A JP2000118379A JP2000118379A JP2001302222A JP 2001302222 A JP2001302222 A JP 2001302222A JP 2000118379 A JP2000118379 A JP 2000118379A JP 2000118379 A JP2000118379 A JP 2000118379A JP 2001302222 A JP2001302222 A JP 2001302222A
- Authority
- JP
- Japan
- Prior art keywords
- ammonium polyphosphate
- melamine
- weight
- fluidity
- improved fluidity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920001276 ammonium polyphosphate Polymers 0.000 title claims abstract description 84
- 239000004114 Ammonium polyphosphate Substances 0.000 title claims abstract description 70
- 235000019826 ammonium polyphosphate Nutrition 0.000 title claims abstract description 70
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical group NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims abstract description 23
- 150000007974 melamines Chemical class 0.000 claims abstract description 15
- 238000002156 mixing Methods 0.000 claims abstract description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 16
- 229920000877 Melamine resin Polymers 0.000 claims description 12
- 229910021529 ammonia Inorganic materials 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 9
- 239000013078 crystal Substances 0.000 claims description 5
- YSRVJVDFHZYRPA-UHFFFAOYSA-N melem Chemical compound NC1=NC(N23)=NC(N)=NC2=NC(N)=NC3=N1 YSRVJVDFHZYRPA-UHFFFAOYSA-N 0.000 claims description 5
- 150000007522 mineralic acids Chemical class 0.000 claims description 4
- 150000007524 organic acids Chemical class 0.000 claims description 4
- YZEZMSPGIPTEBA-UHFFFAOYSA-N 2-n-(4,6-diamino-1,3,5-triazin-2-yl)-1,3,5-triazine-2,4,6-triamine Chemical group NC1=NC(N)=NC(NC=2N=C(N)N=C(N)N=2)=N1 YZEZMSPGIPTEBA-UHFFFAOYSA-N 0.000 claims description 3
- 241000219112 Cucumis Species 0.000 claims description 3
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 claims description 3
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 claims description 3
- 239000007795 chemical reaction product Substances 0.000 claims description 3
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- 239000011248 coating agent Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 238000011156 evaluation Methods 0.000 description 7
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 6
- 239000003063 flame retardant Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- ZQKXQUJXLSSJCH-UHFFFAOYSA-N melamine cyanurate Chemical compound NC1=NC(N)=NC(N)=N1.O=C1NC(=O)NC(=O)N1 ZQKXQUJXLSSJCH-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- ZFSLODLOARCGLH-UHFFFAOYSA-N isocyanuric acid Chemical compound OC1=NC(O)=NC(O)=N1 ZFSLODLOARCGLH-UHFFFAOYSA-N 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- GUSFEBGYPWJUSS-UHFFFAOYSA-N pentaazanium;[oxido(phosphonatooxy)phosphoryl] phosphate Chemical compound [NH4+].[NH4+].[NH4+].[NH4+].[NH4+].[O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O GUSFEBGYPWJUSS-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- CNPURSDMOWDNOQ-UHFFFAOYSA-N 4-methoxy-7h-pyrrolo[2,3-d]pyrimidin-2-amine Chemical compound COC1=NC(N)=NC2=C1C=CN2 CNPURSDMOWDNOQ-UHFFFAOYSA-N 0.000 description 1
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- DLYUQMMRRRQYAE-UHFFFAOYSA-N phosphorus pentoxide Inorganic materials O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229940005657 pyrophosphoric acid Drugs 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- JMHCCAYJTTWMCX-QWPJCUCISA-M sodium;(2s)-2-amino-3-[4-(4-hydroxy-3,5-diiodophenoxy)-3,5-diiodophenyl]propanoate;pentahydrate Chemical compound O.O.O.O.O.[Na+].IC1=CC(C[C@H](N)C([O-])=O)=CC(I)=C1OC1=CC(I)=C(O)C(I)=C1 JMHCCAYJTTWMCX-QWPJCUCISA-M 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Landscapes
- Fireproofing Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は難燃剤として有用な
流動性の向上したポリリン酸アンモニウムおよびその製
造方法に関する。さらに詳しくは、ポリリン酸アンモニ
ウムに微量のメラミンモノマーもしくはメラミン誘導体
を添加、混合して得られる、ポリリン酸アンモニウムの
二次凝集を防ぎ、流動性が向上したポリリン酸アンモニ
ウムおよびその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ammonium polyphosphate useful as a flame retardant and having improved fluidity, and a method for producing the same. More specifically, the present invention relates to an ammonium polyphosphate obtained by adding and mixing a trace amount of a melamine monomer or a melamine derivative to ammonium polyphosphate, preventing secondary aggregation of ammonium polyphosphate and improving fluidity, and a method for producing the same.
【0002】[0002]
【従来の技術】近年、ポリリン酸アンモニウム(以下、
APPと略すことがある)は、白色微粉末であることか
ら着色に対する自由度に優れ、合成樹脂に添加しても機
械的物性の低下が少なく、しかも有毒なハロゲン系ガス
を発生しない難燃剤として注目を浴びている。しかしな
がら、該APPを扱う場合、流動性が悪く、粉末が凝集
して装置に付着し、扱いにくいという問題点があった。
また、APPを熱可塑性樹脂に配合する場合、微粉末で
あるために樹脂中に均一に分散しにくいという分散性の
問題があった。そのため、該APPを難燃剤として熱可
塑性樹脂に配合した組成物を用いて成形すると、得られ
る成形品は部分的に難燃剤濃度が異なり、そのため難燃
性にバラツキが出る可能性が有った。2. Description of the Related Art In recent years, ammonium polyphosphate (hereinafter, referred to as ammonium polyphosphate) has been used.
APP is sometimes referred to as APP) because it is a white fine powder and has excellent freedom in coloring. Even when it is added to a synthetic resin, its mechanical properties are small, and it does not generate toxic halogen-based gas. It is getting attention. However, when handling the APP, there is a problem that the fluidity is poor and the powder is agglomerated and adheres to the device, making it difficult to handle.
In addition, when APP is mixed with a thermoplastic resin, there is a problem of dispersibility that it is difficult to disperse uniformly in the resin because of the fine powder. Therefore, when molding was performed using a composition in which the APP was blended with a thermoplastic resin as a flame retardant, the resulting molded article partially had a different flame retardant concentration, and thus there was a possibility that the flame retardancy would vary. .
【0003】そこで、従来から上記の問題点を解決する
ために該APPの表面を各種ポリマーや改質剤でコーテ
ィングもしくはマイクロカプセル化する方法が提案され
ている。APPの流動性すなわち集塊性を改良する方法
として、特開平3−131508号公報には、APPを
硬化性シリコン樹脂でコーティング処理する方法が開示
されている。また、APPを被覆する方法として、US
4467056号公報にはメラミン/ホルムアルデヒド
樹脂で、US4514328号公報にはエポキシ樹脂
で、DE3438096号公報および特開昭61−98
722号公報には尿素樹脂で、特開昭61−98721
号公報にはポリウレタンで、特開昭61−98719号
公報にはポリカルボジイミドで、US4347334号
公報にはフェノール樹脂でポリリン酸アンモニウムをマ
イクロカプセル化し流動性を改良する方法が開示されて
いる。[0003] Therefore, in order to solve the above-mentioned problems, a method of coating or microencapsulating the surface of the APP with various polymers and modifiers has been conventionally proposed. As a method of improving the fluidity, that is, the agglomeration property of APP, JP-A-3-131508 discloses a method of coating APP with a curable silicone resin. As a method for coating APP, US Pat.
No. 4,467,056 discloses a melamine / formaldehyde resin, and US Pat. No. 4,514,328 discloses an epoxy resin, which is disclosed in DE 3438096 and JP-A-61-98.
U.S. Pat. No. 722 discloses a urea resin.
JP-A-61-98719 discloses a method for improving the fluidity by microencapsulating ammonium polyphosphate with a polycarbodiimide and US Pat. No. 4,347,334 with a phenol resin.
【0004】しかしながら、これらの方法は、いずれも
溶液中にコーティング剤をポリリン酸アンモニウムと共
に分散させ、APP表面で該コ−テイング剤を硬化、コ
−テイングさせた後、取り出す方法を採るためにその工
程が複雑でありコストがかかる。また、処理方法によっ
てはAPPを取り巻いたコーティング樹脂同士で硬化し
てしまい、凝集塊ができることで平均粒子径の増大もし
ばしばある。[0004] However, all of these methods involve dispersing a coating agent in a solution together with ammonium polyphosphate, curing and coating the coating agent on the APP surface, and then removing the coating agent. The process is complicated and costly. Further, depending on the treatment method, the coating resins surrounding the APP are cured with each other, and the average particle diameter often increases due to the formation of agglomerates.
【0005】溶液を使用しない方法として、特開平8−
134455号公報には、流動性、撥水性を改善するた
めに、シリコーンオイルで表面処理された微粉シリカを
含むポリリン酸アンモニウムが開示されている。しかし
ながら、APPの流動性が改善されるのに充分な量の該
微粉シリカを添加すると、ポリリン酸アンモニウムの持
つ難燃性能が損われるといった問題が有った。As a method not using a solution, Japanese Patent Application Laid-Open No.
No. 134455 discloses an ammonium polyphosphate containing finely divided silica surface-treated with silicone oil in order to improve fluidity and water repellency. However, when a sufficient amount of the finely divided silica is added to improve the flowability of APP, there is a problem that the flame retardancy of ammonium polyphosphate is impaired.
【0006】[0006]
【発明が解決しようとする課題】本発明者らは、前記に
掲げた問題点を解決すべく鋭意検討を重ねた。その結
果、APPに特定のメラミン誘導体を極微量添加混合す
ると、得られるポリリン酸アンモニウムは、本来該AP
Pの持つ難燃性能を損なうこと無く、流動性が向上する
ことを見出し、この知見に基づいて本発明を完成した。
以上の記述から明らかなように、本発明の目的はポリリ
ン酸アンモニウムの難燃性を損なうこと無く、流動性を
改善したポリリン酸アンモニウムを提供することであ
る。SUMMARY OF THE INVENTION The present inventors have conducted intensive studies to solve the above-mentioned problems. As a result, when a very small amount of a specific melamine derivative is added to and mixed with APP, the resulting ammonium polyphosphate originally has
It has been found that the fluidity is improved without impairing the flame retardancy of P, and the present invention has been completed based on this finding.
As is apparent from the above description, an object of the present invention is to provide an ammonium polyphosphate having improved fluidity without impairing the flame retardancy of the ammonium polyphosphate.
【0007】[0007]
【課題を解決するための手段】本発明は以下から構成さ
れる。 (1)全体を100重量%とした時に、96〜99.9
5重量%のポリリン酸アンモニウムと4〜0.05重量
%のメラミンモノマーもしくはメラミン誘導体とを混合
することによって得られる流動性の向上したポリリン酸
アンモニウム。The present invention comprises the following. (1) When the whole is 100% by weight, 96 to 99.9.
An ammonium polyphosphate having improved fluidity obtained by mixing 5% by weight of ammonium polyphosphate with 4 to 0.05% by weight of a melamine monomer or melamine derivative.
【0008】(2)ポリリン酸アンモニウムの結晶型が
II型またはV型であることを特徴とする前記第1項記載
の流動性の向上したポリリン酸アンモニウム。(2) The crystal form of ammonium polyphosphate is
2. The ammonium polyphosphate having improved fluidity according to the above item 1, which is a type II or a type V.
【0009】(3)メラミン誘導体が、メラム、メレ
ム、メロン、メラミンとホルムアルデヒドとの反応物、
またはメラミンと無機酸もしくは有機酸との塩およびそ
れらの混合物であることを特徴とする前記第1項もしく
は第2項のいずれか1項記載の流動性の向上したポリリ
ン酸アンモニウム。(3) The melamine derivative is a melam, melem, melon, a reaction product of melamine and formaldehyde,
3. The ammonium polyphosphate having improved fluidity according to any one of the above items 1 or 2, which is a salt of melamine and an inorganic acid or an organic acid and a mixture thereof.
【0010】(4)流動性の向上したポリリン酸アンモ
ニウムが20゜〜40゜の安息角を有する前記第1項記
載の流動性の向上したポリリン酸アンモニウム。(4) The ammonium polyphosphate having improved fluidity according to the above item 1, wherein the ammonium polyphosphate having improved fluidity has an angle of repose of 20 ° to 40 °.
【0011】(5)全体を100重量%とした時に、9
6〜99.95重量%のポリリン酸アンモニウムと4〜
0.05重量%のメラミンモノマーもしくはメラミン誘
導体とを空気もしくはアンモニア雰囲気下、10分〜3
時間混合することを特徴とする流動性の向上したポリリ
ン酸アンモニウムの製造方法。(5) When the whole is 100% by weight, 9%
6-99.95% by weight of ammonium polyphosphate and 4-
0.05% by weight of melamine monomer or melamine derivative in air or ammonia atmosphere for 10 minutes to 3 minutes
A method for producing ammonium polyphosphate having improved fluidity, comprising mixing for a period of time.
【0012】本発明に用いるポリリン酸アンモニウム
は、一般式 H(n-m)+2(NH4)mPnO3n+1(式中、nは20〜20
00の数であり、mはn+2という最大値を有し、m/
nは0.9〜1.1の間にある)または(NH4)n+2P
nO3n+1(式中、nは20〜2000の数を表す)で表
される化合物であり、nの値が充分に大きいときは、メ
タリン酸の式(NH4PO3)nに近似できる化合物であ
る。[0012] Ammonium polyphosphate used in the present invention have the general formula H (nm) +2 (NH 4 ) m P n O 3n + 1 ( wherein, n 20 to 20
00, where m has a maximum value of n + 2 and m /
n is between 0.9 and 1.1) or (NH 4) n + 2 P
n O 3n + 1 (where n represents a number from 20 to 2,000), and when the value of n is sufficiently large, it approximates the formula (NH 4 PO 3 ) n of metaphosphoric acid It is a compound that can be made.
【0013】該ポリリン酸アンモニウムには、一般にI
型〜VI型までの結晶型が有ることが知られているが、本
発明に好適に用いられる結晶型はII型とV型である。該
結晶型のスペクトルデータは、シー・ワイ・シェン(C.
Y. Shen)らによるジャーナルオブ アメリカン ケミカル
ソサイアティ(Journal of American Chemical Societ
y), 91, p62-67(1969)、およびKjell R. Waestadらによ
るジャーナル オブ アグリカルチャラル アンド フード
ケミストリ(Journal of Agricultural and Food Chem
istry), vol.24, No.2, p412-415(1978)に記載されてい
る。The ammonium polyphosphate generally comprises I
It is known that there are crystal forms from Form to Form VI, but the crystal forms preferably used in the present invention are Form II and Form V. The spectrum data of the crystal form is obtained from Shi Wai Shen (C.
Journal of American Chemical Societ by Y. Shen et al.
y), 91, p62-67 (1969), and the Journal of Agricultural and Food Chemistry by Kjell R. Waestad et al.
istry), vol. 24, No. 2, p412-415 (1978).
【0014】本発明に用いられるポリリン酸アンモニウ
ムは、平均粒子径が40μm以下のものが実用的であり、
好ましい。平均粒子径が40μmよりも大きい場合でも、
本発明の方法により流動性は向上するが、該ポリリン酸
アンモニウムを熱可塑性樹脂用の難燃剤として使用する
と、該樹脂中での分散性が悪くなり、良好な難燃性を得
られなかったり、得られた樹脂を用いて成形すると得ら
れる成形品の機械的物性を低下させる可能性がある。ま
た、本発明に用いられるポリリン酸アンモニウムを25
℃の水90ml中に10g分散させたとき、1時間の溶解量
が1g以下であるものが好適である。The ammonium polyphosphate used in the present invention has a practical average particle diameter of 40 μm or less.
preferable. Even when the average particle size is larger than 40 μm,
Although the fluidity is improved by the method of the present invention, when the ammonium polyphosphate is used as a flame retardant for a thermoplastic resin, the dispersibility in the resin becomes poor, and good flame retardancy cannot be obtained, When molding is performed using the obtained resin, there is a possibility that the mechanical properties of the obtained molded product are reduced. Further, the ammonium polyphosphate used in the present invention is 25%.
When 90 g of water is dispersed in 90 ml of water at 10 ° C., it is preferable that the amount dissolved per hour is 1 g or less.
【0015】このような特性を備えたポリリン酸アンモ
ニウムは、市販品として、ホスタフラムAP−422
(クラリアント社製)、FR−CROS484(ブーデ
ンハイム社製)、テラージュS20(チッソ(株)製)
を挙げることができるほか、公知の方法によっても得る
ことができる。公知の方法としては、例えば、ほぼ等モ
ル量のオルトリン酸アンモニウムと五酸化リンとをガス
状アンモニアの存在下でかつ反応物の同時運動下に温度
170〜350℃に加熱する方法を挙げることができる。Ammonium polyphosphate having such properties is commercially available as Hostaflam AP-422.
(Manufactured by Clariant), FR-CROS484 (manufactured by Boudenheim), Terage S20 (manufactured by Chisso Corporation)
In addition to the above, it can also be obtained by a known method. Known methods include, for example, the addition of approximately equimolar amounts of ammonium orthophosphate and phosphorus pentoxide in the presence of gaseous ammonia and simultaneous movement of the reactants.
A method of heating to 170 to 350 ° C. can be mentioned.
【0016】本発明の流動性の向上したポリリン酸アン
モニウムを得るためには、メラミンモノマーまたはメラ
ミン誘導体を前記ポリリン酸アンモニウムに配合する。
該メラミン誘導体としては、メラミンモノマーを注意深
く350℃以上に加熱することによって得られるメラム
(C6H9N11)、メレム(C6H9N10)、さらに600
℃以上にメレムを加熱することによりメレム3分子から
3分子の脱アンモニア化によって得られるメロン(C18
H18N27)を挙げることができる。さらに、メラミンと
ホルムアルデヒドとの反応生成物、メラミンと有機酸も
しくは無機酸との塩も好適に使用できる。該有機酸とし
ては、シアヌル酸やイソシアヌル酸が好適に使用でき、
該無機酸としては硫酸、燐酸、およびピロ燐酸が好適に
使用できる。本発明にあってはメラミンモノマーおよび
該メラミン誘導体を単独もしくは混合して使用すること
ができる。In order to obtain an ammonium polyphosphate having improved fluidity according to the present invention, a melamine monomer or a melamine derivative is added to the ammonium polyphosphate.
The melamine derivative includes melam (C 6 H 9 N 11 ), melem (C 6 H 9 N 10 ), and 600, which are obtained by carefully heating a melamine monomer to 350 ° C. or more.
Melon (C 18) obtained by deammonification of three molecules of melem by heating the melem above 3 ° C.
H 18 N 27 ). Further, a reaction product of melamine and formaldehyde, and a salt of melamine with an organic acid or an inorganic acid can also be suitably used. As the organic acid, cyanuric acid and isocyanuric acid can be suitably used,
As the inorganic acid, sulfuric acid, phosphoric acid, and pyrophosphoric acid can be suitably used. In the present invention, the melamine monomer and the melamine derivative can be used alone or as a mixture.
【0017】本発明の流動性の向上したポリリン酸アン
モニウムは、ポリリン酸アンモニウムに、メラミンモノ
マーまたは前述したメラミン誘導体を混合物全量に対し
て、0.05〜4重量%、好ましくは0.1〜2重量%
添加し、攪拌、混合することによって得ることができ
る。0.05重量%未満の時は、ポリリン酸アンモニウ
ムの流動性が向上しない場合が有り、4重量%を越えて
混合しても流動性の向上効果が飽和し、それ以上の効果
の向上が認められず、さらに本来ポリリン酸アンモニウ
ムが持つ難燃性能の低下を引き起こす場合がある。The ammonium polyphosphate having improved fluidity according to the present invention comprises 0.05 to 4% by weight, preferably 0.1 to 2% by weight, based on the total amount of the mixture of ammonium polyphosphate and a melamine monomer or the aforementioned melamine derivative. weight%
It can be obtained by adding, stirring and mixing. If the content is less than 0.05% by weight, the fluidity of ammonium polyphosphate may not be improved. Even if the content exceeds 4% by weight, the effect of improving the fluidity is saturated, and the effect is further improved. In some cases, the flame retardant performance of ammonium polyphosphate may be reduced.
【0018】また、撹拌、混合するとき、メラミンモノ
マーまたはメラミン誘導体の分解もしくは昇華温度以下
に加熱しても良い。加熱する場合にはポリリン酸アンモ
ニウムからアンモニアが脱離することを防ぐために、ア
ンモニアを通気し、加熱器内をアンモニア雰囲気に保つ
ことが好ましい。アンモニア通気量は、その温度でポリ
リン酸アンモニウムから脱離するアンモニアの分圧より
わずかに多ければよく、該アンモニア分圧は、クラウシ
ス−クラペイロンの式から求められた前記シェンらの文
献に記載されている蒸気圧の式logP=8.207-3230/(273.1
5+T)(ここでPはアンモニアの蒸気圧(mmHg)であり、Tは
温度(℃)である)から計算した値である3Pa〜100
kPa程度でよい。微量な流量を制御するのが困難な時
は他のガスと混合して通気しても良い。When stirring and mixing, the mixture may be heated to a temperature lower than the decomposition or sublimation temperature of the melamine monomer or melamine derivative. In the case of heating, in order to prevent ammonia from desorbing from ammonium polyphosphate, it is preferable to ventilate ammonia and keep the inside of the heater in an ammonia atmosphere. The ammonia aeration may be slightly greater than the partial pressure of ammonia desorbed from the ammonium polyphosphate at that temperature, and the ammonia partial pressure may be as described in the aforementioned Shen et al. Equation of vapor pressure logP = 8.207-3230 / (273.1
5 + T) (where P is the vapor pressure of ammonia (mmHg) and T is the temperature (° C.)).
It may be about kPa. When it is difficult to control a small amount of flow, it may be mixed with another gas and ventilated.
【0019】本発明の流動性が向上したポリリン酸アン
モニウムを得るための装置は、当業者が均一な混合を意
図して用意できるものであればとくに制限はなく、市販
のボールミル、V型ブレンダー、リボンブレンダー、ス
クリューブレンダー、ニーダー等の混合機が使用でき、
場合により加熱装置を備えた機器も使用できる。The apparatus for obtaining the ammonium polyphosphate having improved fluidity of the present invention is not particularly limited as long as it can be prepared by a person skilled in the art with a view to uniform mixing, and a commercially available ball mill, V-type blender, Mixers such as ribbon blenders, screw blenders, and kneaders can be used,
Optionally, equipment with a heating device can also be used.
【0020】[0020]
【実施例】本発明を具体的に説明するために、以下に実
施例、比較例を示すが、本発明はこれによって限定され
るものではない。また、本発明に係わる原材料および評
価方法は次の手法により行った。EXAMPLES Examples and comparative examples will be shown below to specifically explain the present invention, but the present invention is not limited by these examples. The raw materials and evaluation method according to the present invention were performed by the following methods.
【0021】(1)原材料 (i)メラミン:(ユカメラミン:三菱化学社製)、(i
i)シアヌル酸メラミン:(メラミンシアヌレートMC-44
0:日産化学社製)、(iii)ポリリン酸アンモニウム1
(ホスタフラムAP-422:クラリアント社製)、(iv)ポリ
リン酸アンモニウム2(FRCROS−484:ブーデンハイム
社製)、(v)ポリリン酸アンモニウム3(テラージュS
20:チッソ(株)社製)(1) Raw materials (i) Melamine: (Ucamamine: manufactured by Mitsubishi Chemical Corporation), (i)
i) Melamine cyanurate: (Melamine cyanurate MC-44
0: Nissan Chemical Industries, Ltd.), (iii) Ammonium polyphosphate 1
(Hostafram AP-422: Clariant), (iv) Ammonium polyphosphate 2 (FRCROS-484: Bodenheim), (v) Ammonium polyphosphate 3 (Terage S)
20: Chisso Corporation)
【0022】(2)評価方法 (i)流動性の評価 ロート角度40゜、ロート孔径15mmのステンレス製
のロートを用い、実施各例、比較各例で得られた試料粉
体を該ロートに入れ、水平の板の上に堆積させ、形成さ
れた円錐底面の半径と高さから安息角を測定した。この
安息角の数値が小さい方が流動性は良好であることを示
す。また、試料をロートに移した際のロートのつまり発
生についても調べた。(2) Evaluation method (i) Evaluation of fluidity Using a stainless steel funnel having a funnel angle of 40 ° and a funnel hole diameter of 15 mm, the sample powder obtained in each of the examples and comparative examples was put into the funnel. The angle of repose was measured from the radius and height of the bottom of the cone formed on a horizontal plate. The smaller the value of the angle of repose, the better the fluidity. In addition, the occurrence of funnel clogging when the sample was transferred to the funnel was also examined.
【0023】実施例1 ポリリン酸アンモニウム1に、メラミンを全体の1重量
%になるように添加してV型ブレンターを使用して、2
5℃で1時間混合し、混合処理したポリリン酸アンモニ
ウムを得た。得られた混合処理したポリリン酸アンモニ
ウムを用いて、上記評価方法により、流動性の評価を行
った。その結果を表1に示した。EXAMPLE 1 Melamine was added to ammonium polyphosphate 1 so as to make up 1% by weight of the total, and a V-type blender was used to obtain 2% by weight.
The mixture was mixed at 5 ° C. for 1 hour to obtain a mixed ammonium polyphosphate. Using the obtained mixed-treated ammonium polyphosphate, fluidity was evaluated by the above evaluation method. The results are shown in Table 1.
【0024】実施例2 ポリリン酸アンモニウム2と全体の0.5重量%になる
ようにメラミンとを、加熱装置を備えた内容積5リット
ルのニーダーに装入し、150℃で1時間アンモニア雰
囲気中で混合し、混合処理したポリリン酸アンモニウム
を得た。得られた混合処理したポリリン酸アンモニウム
を用いて、上記評価方法により、流動性の評価を行っ
た。その結果を表1に示した。Example 2 Ammonium polyphosphate 2 and melamine were added to a 5 liter internal volume kneader equipped with a heating device so as to be 0.5% by weight of the whole, and were placed in an ammonia atmosphere at 150 ° C. for 1 hour. To obtain a mixed ammonium polyphosphate. Using the obtained mixed-treated ammonium polyphosphate, fluidity was evaluated by the above evaluation method. The results are shown in Table 1.
【0025】実施例3 ポリリン酸アンモニウム3、シアヌル酸メラミンを全体
の1重量%および」メラミンを全体の2重量%になるよ
うに、加温装置のついたリボンブレンダーにそれぞれ装
入して、40℃で2時間空気中で混合し、混合処理した
ポリリン酸アンモニウムを得た。得られた混合処理した
ポリリン酸アンモニウムを用いて、上記評価方法によ
り、流動性の評価を行った。その結果を表1に示した。Example 3 Ammonium polyphosphate 3, melamine cyanurate 1% by weight and melamine 2% by weight were charged into a ribbon blender equipped with a heating device, respectively, to obtain 40% by weight. The mixture was mixed at room temperature for 2 hours in the air to obtain a mixed ammonium polyphosphate. Using the obtained mixed-treated ammonium polyphosphate, fluidity was evaluated by the above evaluation method. The results are shown in Table 1.
【0026】比較例1 メラミンを添加しないポリリン酸アンモニウム2の安息
角並びにロートのつまりについて評価した。その結果を
表1に示した。Comparative Example 1 The angle of repose and the clogging of the funnel of ammonium polyphosphate 2 to which melamine was not added were evaluated. The results are shown in Table 1.
【0027】比較例2 ポリリン酸アンモニウム1と、メラミンシアヌレートを
全体の0.03重量%になるように、加熱装置を備えた内容
積5リットルのニーダーに挿入し、40℃で2時間、空
気雰囲気中で混合してサンプルを得た。得られたサンプ
ルを用いて、上記評価方法により、流動性の評価を行っ
た。その結果を表1に示した。COMPARATIVE EXAMPLE 2 Ammonium polyphosphate 1 and melamine cyanurate were inserted into a kneader having an inner volume of 5 liters equipped with a heating device so as to be 0.03% by weight of the whole, and were placed in an air atmosphere at 40.degree. To obtain a sample. Using the obtained sample, fluidity was evaluated by the above-described evaluation method. The results are shown in Table 1.
【0028】[0028]
【表1】 [Table 1]
【0029】[0029]
【発明の効果】本発明のポリリン酸アンモニウムは、メ
ラミンもしくはメラミン誘導体およびそれらの混合物を
ポリリン酸アンモニムに微量に添加して混合するだけで
流動性、取り扱い性が大幅に改善されたポリリン酸アン
モニウムである。また、本発明のポリリン酸アンモニウ
ムは、合成樹脂等に難燃剤として使用する際にその取り
扱い性、流動性が良好であるため、該樹脂中に均一に分
散させることができ、さらに添加剤の量がごく微量であ
るため、本来ポリリン酸アンモニウムが持つ難燃性能を
阻害することがなく、良好な難燃性を付与することがで
きる。The ammonium polyphosphate of the present invention is an ammonium polyphosphate whose flowability and handleability are greatly improved only by adding a small amount of melamine or a melamine derivative and a mixture thereof to ammonium polyphosphate and mixing. is there. Further, the ammonium polyphosphate of the present invention has good handleability and fluidity when used as a flame retardant in a synthetic resin or the like, so that it can be uniformly dispersed in the resin, and the amount of the additive Since the amount is very small, it is possible to impart good flame retardancy without impairing the flame retardancy inherent to ammonium polyphosphate.
Claims (5)
9.95重量%のポリリン酸アンモニウムと4〜0.0
5重量%のメラミンモノマーもしくはメラミン誘導体と
を混合することによって得られる流動性の向上したポリ
リン酸アンモニウム。(1) When the total content is 100% by weight, 96 to 9
9.95% by weight of ammonium polyphosphate and 4 to 0.0
Ammonium polyphosphate with improved flowability obtained by mixing 5% by weight of a melamine monomer or melamine derivative.
V型の結晶型のものである請求項1記載の流動性の向上
したポリリン酸アンモニウム。2. The method of claim 2, wherein the ammonium polyphosphate is of type II or
The ammonium polyphosphate having improved fluidity according to claim 1, which is a V-type crystal type.
ン、メラミンとホルムアルデヒドとの反応物またはメラ
ミンと無機酸もしくは有機酸との塩およびそれらの混合
物である請求項1もしくは請求項2のいずれか1項記載
の流動性の向上したポリリン酸アンモニウム。3. The method according to claim 1, wherein the melamine derivative is melam, melem, melon, a reaction product of melamine with formaldehyde, a salt of melamine with an inorganic or organic acid, or a mixture thereof. An ammonium polyphosphate having improved fluidity according to the above item.
が、20゜〜40゜の安息角を有するものである請求項
1記載の流動性の向上したポリリン酸アンモニウム。4. The ammonium polyphosphate having improved fluidity according to claim 1, wherein the ammonium polyphosphate having improved fluidity has an angle of repose of 20 ° to 40 °.
9.95重量%のポリリン酸アンモニウムと4〜0.0
5重量%のメラミンモノマーもしくはメラミン誘導体と
を空気もしくはアンモニア雰囲気下、10分〜3時間混
合することを特徴とする流動性の向上したポリリン酸ア
ンモニウムの製造方法。5. When the total content is 100% by weight, 96-9%
9.95% by weight of ammonium polyphosphate and 4 to 0.0
A method for producing ammonium polyphosphate having improved fluidity, comprising mixing 5% by weight of a melamine monomer or a melamine derivative in an air or ammonia atmosphere for 10 minutes to 3 hours.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100420706C (en) * | 2005-03-02 | 2008-09-24 | 杭州捷尔思阻燃化工有限公司 | Preparation method and product of melamine polyphosphate |
JP2009001435A (en) * | 2007-06-19 | 2009-01-08 | Shin Etsu Chem Co Ltd | Method for modifying ammonium polyphosphate |
WO2018181676A1 (en) * | 2017-03-31 | 2018-10-04 | 株式会社Adeka | Flame retardant composition and flame-retardant synthetic resin composition containing same |
CN114806249A (en) * | 2022-04-12 | 2022-07-29 | 广州龙文建材有限公司 | Building fireproof coating and preparation method thereof |
CN115159487A (en) * | 2022-08-05 | 2022-10-11 | 重庆消防安全技术研究服务有限责任公司 | Method for preparing ammonium polyphosphate by using waste dry powder extinguishing agent |
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-
2000
- 2000-04-19 JP JP2000118379A patent/JP2001302222A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100420706C (en) * | 2005-03-02 | 2008-09-24 | 杭州捷尔思阻燃化工有限公司 | Preparation method and product of melamine polyphosphate |
JP2009001435A (en) * | 2007-06-19 | 2009-01-08 | Shin Etsu Chem Co Ltd | Method for modifying ammonium polyphosphate |
WO2018181676A1 (en) * | 2017-03-31 | 2018-10-04 | 株式会社Adeka | Flame retardant composition and flame-retardant synthetic resin composition containing same |
JP2018172590A (en) * | 2017-03-31 | 2018-11-08 | 株式会社Adeka | Flame retardant composition and flame-retardant synthetic resin composition containing the same |
CN110337483A (en) * | 2017-03-31 | 2019-10-15 | 株式会社艾迪科 | Flame retardant composition and flame retardant synthetic resin composition containing same |
US11753527B2 (en) | 2017-03-31 | 2023-09-12 | Adeka Corporation | Flame retardant composition and flame-retardant synthetic resin composition containing same |
CN114806249A (en) * | 2022-04-12 | 2022-07-29 | 广州龙文建材有限公司 | Building fireproof coating and preparation method thereof |
CN115159487A (en) * | 2022-08-05 | 2022-10-11 | 重庆消防安全技术研究服务有限责任公司 | Method for preparing ammonium polyphosphate by using waste dry powder extinguishing agent |
CN115159487B (en) * | 2022-08-05 | 2023-08-08 | 重庆消防安全技术研究服务有限责任公司 | Method for preparing ammonium polyphosphate by using waste dry powder extinguishing agent |
CN115850799A (en) * | 2022-12-23 | 2023-03-28 | 山东省海洋化工科学研究院 | Tubular kaolin modified ammonium polyphosphate functional monomer and preparation method thereof |
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